Pregled bibliografske jedinice broj: 616551
Enhancement of phenolic compounds oxidation using laccase from Trametes versicolor in a microreactor
Enhancement of phenolic compounds oxidation using laccase from Trametes versicolor in a microreactor // Biotechnology and bioprocess engineering, 18 (2013), 4; 686-696 doi:10.1007/s12257-012-0688-8 (međunarodna recenzija, članak, znanstveni)
CROSBI ID: 616551 Za ispravke kontaktirajte CROSBI podršku putem web obrasca
Naslov
Enhancement of phenolic compounds oxidation using laccase from Trametes versicolor in a microreactor
Autori
Jurinjak Tušek, Ana ; Tišma, Marina ; Bregović, Valentina ; Ptičar, Ana ; Kurtanjek, Želimir ; Zelić, Bruno
Izvornik
Biotechnology and bioprocess engineering (1226-8372) 18
(2013), 4;
686-696
Vrsta, podvrsta i kategorija rada
Radovi u časopisima, članak, znanstveni
Ključne riječi
microreactor ; oxidation of phenolic compounds ; laccase ; kinetic measurements ; mathematical model
Sažetak
Laccases catalyse the oxidation of a wide range of substrates by a radical-catalyzed reaction mechanism, with a corresponding reduction of oxygen to water in a four-electron transfer process. Due to that, laccases are considered environmentally friendly enzymes, and lately there has been great interest in their use for the transformation and degradation of phenolic compounds. In this work, enzymatic oxidation of catechol and L-DOPA using commercial laccase from Trametes versicolor was performed, in continuously operated microreactors. The main focus of this investigation was to develop a new process for phenolic compounds oxidation, by application of microreactors. For a residence time of 72 s and an inlet oxygen concentration of 0.271 mmol/dm3, catechol conversion of 41.3% was achieved, while approximately the same conversion of L-DOPA (45.0%) was achieved for an inlet oxygen concentration of 0.544 mmol/dm3. The efficiency of microreactor usage for phenolic compounds oxidation was confirmed by calculating the oxidation rates ; in the case of catechol oxidation, oxidation rates were in the range from 76.101 to 703.935 g/dm3/d (18–167 fold higher, compared to the case in a macroreactor). To better describe the proposed process, kinetic parameters of catechol oxidation were estimated, using data collected from experiments performed in a microreactor. The maximum reaction rate estimated in microreactor experiments was two times higher than one estimated using the initial reaction rate method from experiments performed in a cuvette. A mathematical model of the process was developed, and validated, using data from independent experiments.
Izvorni jezik
Engleski
Znanstvena područja
Biotehnologija
Napomena
Ovaj se tekst temelji na radu koji je financirala Hrvatska zaklada za znanost.
POVEZANOST RADA
Ustanove:
Prehrambeno-biotehnološki fakultet, Zagreb,
Prehrambeno-tehnološki fakultet, Osijek,
Fakultet kemijskog inženjerstva i tehnologije, Zagreb
Profili:
Marina Tišma
(autor)
Ana Jurinjak Tušek
(autor)
Bruno Zelić
(autor)
Želimir Kurtanjek
(autor)
Citiraj ovu publikaciju:
Časopis indeksira:
- Current Contents Connect (CCC)
- Web of Science Core Collection (WoSCC)
- Science Citation Index Expanded (SCI-EXP)
- SCI-EXP, SSCI i/ili A&HCI
- Scopus